Process for preparing methylene diphenylamines by partial neutralization of acidic methylene diphenylamines

ABSTRACT

Disclosed herein is a process for preparing a reaction product containing methylene diphenylamine, comprising reacting aniline and formaldehyde in the presence of an acid catalyst wherein the acid level of the resulting reaction mixture is reduced during digestion of the reaction mixture.

FIELD OF THE INVENTION

The present invention relates to the preparation of polyamines. Morespecifically, the invention relates to a process for preparing methylenediphenylamines by partial neutralization of acidic aniline/aldehydereaction products.

BRIEF DESCRIPTION OF THE PRIOR ART

Generally, it is known in the art to react aniline with formaldehyde inthe presence of an acid such as hydrochloric acid to produce methylenediphenylamines. Of particular interest here is the methylenediphenylamines which are useful in the production of polyisocyanateswhich in turn are useful in the preparation of polyurethane/polyureafoams. Lately, the color of foams has become one of the requirements forjudging the quality of foams. Foams which are otherwise acceptable canbe rejected because of dark color.

Poor quality of the methylene diphenylamines and consequently thepolyisocyanates, at least in part, has been blamed for the discolorationin foams. Hence, a number of improvements in this area have been made inthe preparation of higher quality methylene diphenylamines.

U.S. Pat. No. 4,792,624 discloses that polymethylene polyphenylpolyisocyanates of improved color can be obtained from certainpolyamines which are prepared by the following process. The processcomprises condensing aniline and formaldehyde in the presence of an acidcatalyst and is characterized by adding a minor proportion of apolyamine mixture comprising di(aminophenyl)methanes and oligomericpolymethylene polyphenyl polyamines, (collectively known as polymericMDA) to an intermediate stage of the condensation reaction where thevarious intermediately formed aminobenzoylamines are present.

U.S. Pat. No. 4,465,639 discloses the production of polymethylenepolyphenyl polyamines by addition of controlled amounts of water to thereaction mixture produced by phosgenation of a mixture of polymethylenepolyphenyl polyamines (and the like polyamines produced by condensationof formaldehyde and aromatic amines) prior to a complete removal ofexcess phosgene. The corresponding polymethylene polyphenylpolyisocyanate is said to have significantly improved properties such ascolor of the polyisocyanates.

U.S. Pat. No. 4,259,526 discloses a process for the preparation ofmixtures of polyamines of the polyamino-polyaryl-polymethylene typewhereby the proportion of the ortho-substituted products aresubstantially increased. This increase is brought about by adding theacid catalyst in two stages by reacting an aromatic amine withformaldehyde in the presence of an aqueous acid catalyst, or subjectinga condensate which has been obtained from an aromatic amine andformaldehyde in the absence of a catalyst to a first rearrangement inthe presence of an aqueous acid catalyst, followed by adding aqueousacid catalyst to the resulting mixture, and then rearranging theintermediates by heating the mixture to 75 to 150 degrees centigrade.This mixture of polyamines is thereafter recovered.

By the present invention, there is provided another process forpreparing polyamines which upon phosgenation produce polyisocyanates oflight color.

SUMMARY OF THE INVENTION

The present invention encompasses a process for preparing a reactionproduct containing methylene diphenylamine, comprising reacting anilineand formaldehyde in the presence of an acid catalyst; reducing the acidlevel of the resulting reaction mixture during digestion of the reactionmixture, followed by completely neutralizing the reaction product afterfurther digestion. Isocyanates corresponding to the polyamines andreaction products thereof, e.g., foams are also encompassed by thepresent invention.

In the present embodiment of the invention the process for preparing thereaction product containing methylene diphenylamine comprises reactinganiline with a formaldehyde in the presence of hydrochloric acid;partially neutralizing the reaction product with sodium hydroxide duringthe digestion stage of the reaction, followed by completely neutralizingthe reaction product after the digestion.

U.S. Pat. No. 4,259,526 which discloses typical aniline and formaldehydereactions in the presence of an acid is incorporated herein by referencesubject to modifications in accordance with the present invention, asdescribed more fully hereunder.

DETAILED DESCRIPTION OF THE INVENTION

In accordance with the invention, the reaction product containingmethylene diphenylamines of the claimed invention is characterized bylow levels of certain impurities. It is believed that increasing levelsof these impurities darken the color of polyisocyanates derived fromsaid amines. Generally, methylene diphenylamines can be prepared byreacting aniline with formaldehyde in the ratio of 1.6 to 8.0 andpreferably 1.6 to 5.0, in the presence of an acid such as hydrochloricacid.

The amount and type of the acid useful herein is that which caneffectively catalyze the subject reaction. The useful acids can be theart-known acids disclosed in the prior art cited above. Illustrative butnon-limiting examples of the useful acids include water soluble acidshaving pKa values below 2.5 and preferably below 1.5. Specific examplesinclude hydrochloric acid which is preferred, hydrobromic acid, sulfuricacid, triflouroacetic acid, methanesulfonic acid, phosphoric acid,formic acid, acetic acid, citric acid and the like. Typically, the acidlevel is about 10% to 100% and preferably 25% to 50% (molar) based onthe aniline. The acid can be added separately or admixed with aniline ina reaction vessel which is usually referred to as "a mix reactor", atthe "initial stage" of the reaction. As would be realized, the acid saltof the aniline can be reacted with the formaldehyde.

The process of this invention may entail split addition of the reagents.For example, the initial stage of the reaction may be performed in twostages in which portions of the formaldehyde are added in stages.

The reaction, at the initial/condensation stage takes place at atemperature of 0° C. to 100° C. and preferably 35° C. to 45° C., atatmospheric pressure and over a period of time sufficient to formintermediates of the reaction product (aminobenzylamines and the like).The period of time can be from about 5 seconds to 60 minutes andpreferably 15 minutes to 45 minutes. The reaction can be conducted inone or more reaction vessels, and the progress of the reaction can bemonitored by conventional analytical techniques.

At the end of the condensation stage, the reaction mixture is admittedto the digestion stage. By the term "digestion" is meant the stage atwhich the intermediate aminobenzylamines rearrange to form methylenediphenylamines and polymethylene polyphenylamine. It is a distinctfeature of the invention that the process for preparing the methylenediphenylamine comprises the step of reducing the acid level of thereaction mixture during digestion. The acid level is reduced to a levelsufficient to effect the rearrangement of the aminobenzylamine over thedigestion temperature and residence time described hereunder. Thereduction in acid level can be effected by partially neutralizing thereaction mixture to the desired acid level, during the digestion stage.In accordance with the invention, less than the stoichiometric amount ofa base required to neutralize the acid is employed. This amount of thebase can be from about 10% to 90% and preferably 70 to 80 molar percentbased on the amount of acid catalyst employed. The useful base is thatwhich can effectively neutralize the acids described hereinabove. Thebase can be an art-known one such as disclosed in the prior art citedabove. The useful base can be selected from the group consisting ofsodium hydroxide, potassium hydroxide and the like. Typically, thedigestion stage is conducted at an elevated temperature of about 60° C.to 200° C. and preferably 90° C. to 160° C., at a pressure sufficient tocontrol boiling of the reaction mixture, for a period of time (residencetime) sufficient to effect the rearrangement of aminobenzylamines intomethylene diphenylamines. Typically the residence time is from about 60minutes to 400 minutes and preferably 100 minutes to 240 minutes. In amulti-vessel, continuous digestion process the partial neutralization iscarried out continuously at a point in the process where the reactionmixture has been digested for from 10% to 90% and preferably from 40% to60% of the total digestion time. After complete digestion, the remainderof the base is added to fully neutralize the acid.

In the practice of the invention, the reaction product containingmethylene diphenylamine can be used in the preparation of lighter colorisocyanate materials by the reaction of phosgene (phosgenation) with thereaction product containing methylene diphenylamine. The phosgenationreaction can be conducted in the presence of an inert solvent such aschlorobenzene. The polyamines are reacted with phosgene in molar ratiosof 1.5 to 20 moles and preferably about 2.2 to 4.0 moles of phosgene peramine group. Upon completion of the phosgenation, the excess phosgeneand hydrogen chloride formed are separately or simultaneously removed.The phosgenation product which is present after the removal of excessphosgene and HCl is in the form of a solution and may be separated intoa gaseous phase containing volatile compounds having isocyanate groupsand a liquid phase which is substantially crude polyisocyanate. Theliquid phase can be worked up to produce polyisocyanates in a purerstate.

In turn, the lighter color polyisocyanates can be used in thepreparation of lighter color isocyanate reaction products such as foams.In the preparation of the foams, the polyisocyanates are reacted with anisocyanate reactive compound such as art-known polyols orpolyamines, inthe presence of a blowing agent such as carbon dioxide derived from thereaction of the polyisocyanate and water. Art-known auxiliary agents andadditives are usually employed in the preparation of the foams.

The invention is further illustrated but is not intended to be limitedby the following examples in which all parts and percentages are byweight unless otherwise specified.

EXAMPLES Comparative Example

The Process For Preparing Polyamines (Conventional Technique)

In a 2 liter, 4 neck round bottom flask equipped with a mechanicalpaddle stirrer, a reflux condenser, an addition funnel under an inertatmosphere is placed 745 g of aniline. The liquid is cooled using an icebath to ˜20° C., at which time 380 g of 36% HCl is added and theresulting mixture is stirred and cooled to ˜10-20° C. Via the additionalfunnel is added 210 g of 37% formaldehyde while maintaining thetemperature of the reaction mixture below 35° C. The reaction mixture isstirred at this temperature for an additional 15 minutes at which time105 g of 37% formaldehyde is added via the addition funnel. The reactionmixture is then heated to a temperature of 60° C. and stirred for 30minutes, at which time the temperature is raised to achieve reflux andmaintained with reflux for 30 minutes. The reaction mixture is thencooled to 80° C. and 306 g of 50% sodium hydroxide is added. Theresulting reaction mixture is heated to reflux and maintained for 15minutes. The reaction mixture is cooled to 25° C. and poured into alarge separatory funnel. The organic material of the mixture isseparated from the aqueous brine and introduced back into the roundbottom flask. To the flask is then added 750 ml of demineralized waterand under an inert atmosphere the mixture is heated to reflux withstirring. The mixture is then cooled to 25° C. and poured into theseparatory funnel. The organic layer is separated from the aqueous layerand then washed twice with demineralized water. The organic layer isthen poured into a 2 liter round bottom flask equipped with a magneticstirrer and a vacuum source. The organic material is heated to 180° C.at a pressure of 1-3 Torr and maintained at that temperature until theMDA vapors become visible in the condensor separating the flask from thevacuum source. The resulting material is approximately 1 kg of monomericand polymeric methylene diphenyl diamine.

EXAMPLE OF THE PRESENT INVENTION

In a 2 liter, 4 neck round bottom flask equipped with a mechanicalpaddle stirrer, a reflux condenser, an additional funnel under an inertatmosphere is placed 745 g of aniline. The liquid is cooled using an icebath to ˜20° C., at which time 380 g of 36% HCl is added and theresulting mixture is stirred and cooled to ˜10-20° C. Via the additionalfunnel is added 210 g of 37% formaldehyde while maintaining thetemperature of the reaction mixture below 35° C. The reaction mixture isstirred at this temperature for an additional 15 minutes at which time105 g of 37% formaldehyde is then heated to a temperature of 60° C. andstirred for 30 minutes at which time 230 g of 50% sodium hydroxide isadded to the reaction mixture and the temperature is raised to achievereflux and maintained with reflux for 30 minutes. The reaction mixtureis then cooled to 80° C. and 76 g of 50% sodium hydroxide is added. Theresulting reaction mixture is heated to reflux and maintained for 15minutes. The reaction mixture is cooled to 25° C. and poured into alarge separatory funnel. The organic material is separated from theaqueous brine and introduced back into the round bottom flask. To theflask is then added 750 ml of demineralized water under an inertatmosphere. The mixture is heated to reflux with stirring. The mixtureis then cooled to 25° C. and poured into the separatory funnel. Theorganic layer is separated from the aqueous layer and then washed twicewith demineralized water. The organic layer is then poured into a 2liter round bottom flask equipped with a magnetic stirrer and a vacuumsource. The organic material is heated to 180° C. at a pressure of 1-3Torr and maintained at that temperature until MDA vapors become visiblein the condensor separating the flask from the vacuum source. Theresulting material is approximately 1 kg of monomeric and polymericmethylene diphenyl diamine.

Color Properties of Polymethylene Polyphenvl Polyisocyanates PreparedFrom Various Polyamines

    ______________________________________                                        MDA Process        430 nm  520 nm                                             ______________________________________                                        Comparative Process                                                                              0.5     0.1                                                  Process of the invention 0.4 0.08                                           ______________________________________                                    

The polyisocyanate derived from polyamines which were prepared by theprocess of this invention showed appreciable reduction in colorintensity as measured by an ultraviolet visible spectrophotometer at 430and 520 nanometers.

Although the invention has been described in detail in the foregoing forthe purpose of illustration, it is to be understood that such detail issolely for that purpose and that variations can be made therein by thoseskilled in the art without departing from the spirit and scope of theinvention except as it may be limited by the claims.

What is claimed is:
 1. A process for preparing a reaction productcontaining methylene diphenylamine, comprising reacting aniline andformaldehyde in the presence of catalyst; reducing the acid level of theresulting reaction mixture during digestion of the reaction mixture, andfollowed by completely neutralizing the reaction product afterdigestion.
 2. The process of claim 1 wherein the acid is hydrochloricacid.
 3. The process of claim 1 wherein the acid level of the resultingreaction product is reduced by partial neutralization.
 4. The process ofclaim 3 wherein the partial neutralization is conducted at a temperatureof about 50° C. to 200° C.
 5. The process of claim 3 wherein theneutralization is conducted with a base.
 6. The process of claim 3wherein the base is sodium hydroxide.
 7. The process of claim 5 whereinthe base is used for the partial neutralization comprises from 10% to90% of the stoichiometric amount.
 8. The process of claim 3 wherein thepartial neutralization takes place after from 10% to 90% of the totaldigestion time.